Structure and Catalytic Performance of Mg-SBA-15-Supported Nickel Catalysts for CO2 Reforming of Methane to Syngas

被引:66
作者
Zhang, Hui [1 ,2 ]
Li, Meng [2 ]
Xiao, Pufu [2 ]
Liu, Delei [2 ]
Zou, Chang-Jun [2 ]
机构
[1] Southwest Petr Univ, State Key Lab Oil & Gas Reservoir Geol & Exploita, Chengdu 610500, Peoples R China
[2] Southwest Petr Univ, Sch Chem & Chem Engn, Chengdu 610500, Peoples R China
基金
中国国家自然科学基金;
关键词
Carbon dioxide reforming; Methane; Ni; Mg-SBA-15; catalyst; Syngas; SYNTHESIS GAS; CARBON-DIOXIDE; HYDROGEN-PRODUCTION; NI CATALYSTS; STEAM; PROMOTERS; ETHANOL; MG; STABILITY; SUPPORT;
D O I
10.1002/ceat.201300006
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A series of Mg-modified SBA-15 mesoporous silicas with different MgO contents were successfully synthesized by a simple one-pot synthesis method and further impregnated with Ni. The Mg-modified SBA-15 materials and supported Ni catalysts were characterized by N-2 physisorption (BET), X-ray diffraction (XRD), temperature-programmed desorption of CO2 (CO2-TPD), temperature-programmed H-2 reduction (H-2-TPR), and temperature-programmed hydrogenation (TPH) techniques and used for methane dry reforming with CO2. CO2-TPD results proved that the addition of Mg increased the total amount of basic sites which was responsible for the enhanced catalytic activity over the Mg-modified Ni catalyst. The excellent catalytic stability of Ni/8Mg-SBA-15 was ascribed to less coking and higher stability of the Ni particle size due to the introduction of Mg.
引用
收藏
页码:1701 / 1707
页数:7
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